Composition of culture medium is more important than co-culture with hepatic non-parenchymal cells in albumin production activity of primary rat hepatocytes,and the effect was enhanced by hepatocytes spheroid culture in collagen gel

Co-culture of primary rat hepatocytes with hepatic non-parenchymal cells or sinusoidal endothelial cells for albumin production activity as an index of liver-specific function was studied. The co-cultures were effective for the expression and maintenance of albumin production activity. However, the co-culture effect was not observed when we used a suitable culture medium, which had already been reported to be sufficient for albumin production activity. Albumin production of dispersed cells in collagen gel culture was higher than that of spheroid culture. In addition, albumin production of spheroids in collagen gel culture was higher than that of spheroid culture and dispersed cell collagen gel culture with a suitable culture medium. We found that culture medium composition was more important than co-culture for expression and maintenance of albumin production. Furthermore, we found that cell–cell interaction was effective for the expression of albumin production, but heterotypic cell–cell interaction was not necessary.     

西洋参悬浮细胞发酵工艺研究

探讨了西洋参悬浮细胞分步培养与稀土、D-半乳糖和甘露醇等诱导子对悬浮细胞生长及皂甙产量的影响。发现继代4d后换液一次再继续培养获得的培养物,在皂甙产率和糖利用率等方面优于连续培养;D-半乳糖作为诱导子,对悬浮培养的西洋参细胞生长、皂甙产率及皂甙的分泌等方面都有非常明显的促进作用。     

Simultaneous production of hydrogen and bioflocculant by Enterobacter sp. BY-29

Hydrogen and a bioflocculant could be produced simultaneously by anaerobic culture of Enterobacter sp. BY-29. For production of hydrogen and the bioflocculant by cell culture of the bacterium in batch cultures, cultivation at 37 °C in a medium containing glucose as a carbon source and Polypepton as a nitrogen source was found to be suitable. In continuous production of hydrogen and the bioflocculant by cell culture or immobilized cells of the bacterium, the hydrogen production rate and hydrogen yield by the immobilized cells on porous glass beads in stirred and column reactors were higher than those by the cell culture in a stirred reactor. However, production of the bioflocculant by the cell culture was superior to that by the immobilized cells in continuous production.     

Production of a secreted glycoprotein from an inducible promoter system in a perfusion bioreactor

The primary advantage of an inducible promoter expression system is that production of the recombinant protein can be biochemically controlled, allowing for the separation of unique growth and production phases of the culture. During the growth phase, the culture is rapidly grown to high cell density prior to induction without the extra metabolic burden of exogenous protein production, thus minimizing the nonproductive period of the culture. Induction of the culture at high cell density ensures that the volumetric production will be maximized. In this work, we have demonstrated the feasibility of overexpressing a reporter glycoprotein from the inducible MMTV promoter in recombinant Chinese hamster ovary (CHO) cells cultured in a high cell density perfusion bioreactor system. Retention of suspension-adapted CHO cells was achieved by inclined sedimentation. To maximize volumetric production of the culture, we have demonstrated that high cell density must be achieved prior to induction. This operating scheme resulted in a 10-fold increase in volumetric titer over the low density induction culture, corresponding directly to a 10-fold increase in viable cell density during the highly productive period of the culture. The amount of glycoprotein produced in this high cell density induction culture during 26 days was 84-fold greater than that produced in a week long batch bioreactor. Long-term perfusion cultures of the recombinant cell line showed a production instability, a phenomenon that is currently being investigated.     

Expression of a human anti-rabies virus monoclonal antibody in tobacco cell culture

A Nicotiana tabacum cv. Xanthi cell culture was initiated from a transgenic plant expressing a human anti-rabies virus monoclonal antibody. Within 3 months, plant cell suspension cultures were established and recombinant protein expression was examined. The antibody was stably produced during culture growth. ELISA, protein G purification, Western blotting, and neutralization assay confirmed that the antibody was fully processed, with association of light and heavy-chains, and that it was able to bind and neutralize rabies virus. Quantification of antibody production in plant cell suspension culture revealed 30 microg/g of cell dry weight for the highest-producing culture (0.5 mg/L), 3 times higher than from the original transgenic plant. The same production level was observed 3 months after cell culture initiation. Plant cell suspension cultures were successfully grown in a new disposable plastic bioreactor, with a growth rate and production level similar to that of cultures in Erlenmeyer flasks.     

On-line determination of optimum time for switching from growth phase to production phase in tissue plasminogen activator production in a microcarrier cell culture

To maximize the productivity of tissue plasminogen activator (TPA) by a mammalian cell culture, on-line determination of the optimum time to switch from the cell growth phase to the TPA production phase was investigated. By measuring the TPA production activity of the cells during the cell growth culture, it was shown that this optimum time was not necessarily the same as the time at which the cell concentration was maximized, and that the optimum time varied with growth culture batch. The TPA production activity of the cells during the growth culture could be estimated by on-line regression analysis using physiological data of the current state, including the oxygen consumption rate (Io₂) and cell concentration, as well as data from past batches. Applying this on-line estimation, the optimum switching time was determined to be the time at which the TPA production activity of the cells in the growth culture became highest, or higher than a certain value according to determined criteria.     

Influence of culture modes on the microbial production of hyaluronic acid by <Emphasis Type="Italic">Streptococcus zooepidemicus</Emphasis>

The principal objective of this study was to assess the effects of culture modes including batch culture, pulse fed-batch culture, constant feeding rate fed-batch culture, and exponential fed-batch culture on the production of hyaluronic acid (HA) by Streptococcus zooepidemicus. Batch cultures had the highest levels of HA productivity, whereas fed-batch cultures were more favorable with regard to cell growth, and exponential fed-batch cultures evidenced the highest cell concentrations. A two-step culture model was proposed to enhance HA production: an exponential fed-batch culture was conducted prior to 8 h and then sucrose supplementation was applied for 8 h to start the batch fermentation of S. zooepidemicus. HA production and productivity were increased by 36 and 37% in the proposed two-step culture process as compared with that observed in the batch culture, respectively. The proposed two-step culture model can be applied in the production of secondary metabolites, and particularly of the exopolysaccharides.     

Enhanced hyaluronic acid production by a two-stage culture strategy based on the modeling of batch and fed-batch cultivation of Streptococcus zooepidemicus

This study aimed to enhance hyaluronic acid (HA) production by a two-stage culture strategy based on the modeling of batch and fed-batch culture of Streptococcus zooepidemicus. Batch culture had higher specific HA synthesis rate while fed-batch culture had higher specific cell growth rate. The lower specific HA synthesis rate in fed-batch culture resulted from the competition of cell growth for the common precursors at a low substrate concentration. Based on the modeling of batch and fed-batch culture of S. zooepidemicus, a two-stage culture strategy was proposed to enhance HA production. S. zooepidemicus were cultured in a fed-batch mode with sucrose concentration maintained at 1.0+/-0.2g/L during 0-8h and then batch culture was performed during 8-20h with an initial sucrose concentration of 15g/L. With the proposed two-stage culture strategy, HA production was increased to 6.6g/L compared with 5.0g/L in batch culture with the same total sucrose. The enhanced HA production by the proposed two-stage culture strategy resulted from the decreased inhibition of cell growth and the increased transformation rate of sucrose to HA.     

Enhanced taxol production and release in Taxus chinensis cell suspension cultures with selected organic solvents and sucrose feeding

Suspension culture of Taxus chinensis cells was carried out in aqueous-organic two-phase systems for the production and in situ solvent extraction of taxol (paclitaxel). Three organic solvents, hexadecane, decanol, and dibutylphthalate, were tested at 5-20% (v/v) in the culture liquid. All of these solvents stimulated taxol release and the yield per cell, though decanol and higher concentrations of the other two solvents depressed biomass growth significantly. Ten percent dibutylphthalate was the optimal solvent for improving taxol production and release with minimal cell growth inhibition. The time of solvent addition to the culture also affected taxol production, with the addition during the late-log growth phase being most favorable. By feeding sucrose to the culture near the stationary growth phase, the cell growth and taxol production period was extended from 27 to 42 days. The combining of the two-phase culture and sucrose feeding increased the taxol yield by about 6-fold compared with the single-phase batch culture, to 36.0 +/- 3.5 mg/L, with up to 63% taxol released. This study shows that in situ solvent extraction combined with nutrient feeding is an effective process strategy for production and recovery of secondary metabolites in plant cell suspension culture.     

Itaconic acid production using an air-lift bioreactor in repeated batch culture of Aspergillus terreus

Repeated itaconic acid production using an air-lift bioreactor was carried out by three methods—two with cell recycling by means of centrifugation and filtration by a stainless steel filter set inside the bioreactor and one by repeated batch culture without cell recycling. In a flask culture, repeated itaconic acid production was stable for 9 cycles (45 d) and the production rate was 0.47 g/l/h. However, in the air-lift bioreactor, it was difficult to produce itaconic acid in the repeated batch culture with cell recycling for a long period due to a decrease in fluidity resulting from an increase in mycelium concentration. In the method without cell recycling, however, repeated itaconic acid production was stable for 4 cycles (21 d) and the production rate was 0.37 g/l/h.     

悬浮培养CHO 细胞生产重组人促红细胞生成素条件的优化*

目的:通过对贴壁培养CHO细胞筛选驯化,得到高表达的细胞后进行悬浮培养生产重组人促红细胞生成素(rHuEPO)。方法:利用96孔板和24孔板对CHO细胞进行筛选,得到高表达细胞株后进行驯化,使其适合悬浮培养,经过摇瓶扩增后接种到生物反应器中无血清培养,每天监测葡萄糖含量,测rHuEPO表达量。结果:悬浮培养CHO细胞生产rHuEPO,生产周期短,表达量比贴壁培养高出很多,操作方便,减少污染,易于放大,并建立了适合悬浮培养的CHO细胞株,为工业化悬浮培养CHO细胞生产rHuEPO提供了技术基础。结论:经过工艺优化后利用无血清悬浮培养生产促红细胞生成素平均表达量较贴壁培养高,生产周期短,有利于降低生产成本。     

Suspension culture process of MethA tumor cell for the production of heat-shock protein glycoprotein 96: process optimization in spinner flasks

Heat-shock proteins (HSPs) act like "chaperones", making sure that the cell's proteins are in the right shape and in the right place at the right time. Heat-shock protein glycoprotein 96 (gp96) is a member of the HSP90 protein family, which chaperones a number of molecules in protein folding and transportation. Heat-shock protein gp96 serves as a natural adjuvant for chaperoning antigenic peptides into the immune surveillance pathways. Currently, heat-shock protein gp96 was only isolated from murine and human tissues and cell lines. An animal cell suspension culture process for the production of heat-shock protein gp96 by MethA tumor cell was developed for the first time in spinner flasks. Effects of culture medium and condition were studied to enhance the MethA tumor cell density and the production and productivity of heat-shock protein gp96. Initial glucose concentration had a significant effect on the heat-shock protein gp96 accumulation, and an initial glucose level of 7.0 g/L was desirable for MethA tumor cell growth and heat-shock protein gp96 production and productivity. Cultures at an initial glutamine concentration of 3 and 6 mM were nutritionally limited by glutamine. At an initial glutamine concentration of 6 mM, the maximal viable cell density of 19.90 x 10(5) cells/mL and the maximal heat-shock protein gp96 production of 4.95 mg/L was obtained. The initial concentration of RPMI 1640 and serum greatly affected the MethA tumor cell culture process. Specifically cultures with lower initial concentration of RPMI 1640 resulted in lower viable cell density and lower heat-shock protein gp96 production. At an initial serum concentration of 8%, the maximal viable cell density of 19.18 x 10(5) cells/mL and the maximal heat-shock protein gp96 production of 5.67 mg/L was obtained. The spin rate significantly affected the cell culture process in spinner flasks, and a spin rate of 150 rpm was desirable for MethA tumor cell growth and heat-shock protein gp96 production and productivity. Not only the cell density but also the production and productivity of heat-shock protein gp96 attained in this work are the highest reported in the culture of MethA tumor cell. This work offers an effective approach for producing heat-shock protein glycoprotein 96 from the cell culture process. The fundamental information obtained in this study may be useful for the efficient production of heat-shock protein by animal cell suspension culture on a large scale.     

Tropane alkaloid production in Datura stramonium suspension cultures: elicitor and precursor effects

The effects of elicitation, carbon, and nitrogen sources, and precursors on cell growth and tropane alkaloid production in Datura stramonium cell cultures were studied. D. Stramonium cell cultures responded very well to elicitors in the late exponential phase. Addition of cell wall fragments of Phytophotora megasperma (Pmg) enhanced the final tropane alkaloid yield by fivefold compared with control culture. Supply of carbon culture. Supply of carbon and nitrogen sources, at a ratio (C/N) of up to 70, to cell cultures in the early stationary phase, suppressed tropane alkaloid production; whereas C/N rations beyond about 100 increased the final product yield by more than 100% compared to that of the control experiment. Total alkaloid production in the cell culture supplemented with phenylalanine and ornithine was five times higher that that in the control culture. Higher rations of tropine to tropic acid also stimulated alkaloid production. At a ratio of 20, the productivity was seven times higher that that in the control culture. Adding precursors at high concentrations (e.g., 3 to 10 mM) to the cell culture reduced the final cell yield by less than 40%, while elicitation did not affect the cell yield. On the other hand, cell yield in the cultures supplemented with carbon and nitrogen sources was influenced by the C/N ratio. The highest cell yield was obtained at C/N = 70. (c) 1993 Wiley & Sons, Inc.     

Optimization of Vi capsular polysaccharide production during growth of Salmonella enterica serotype Typhi Ty2 in a bioreactor

Vi capsular polysaccharide is synthesized during growth of Salmonella typhi Ty2 and is spontaneously released from the bacterial cells into the culture medium during culture. Vi production was dependent on cell growth and the greater the cell mass the greater the production of Vi. Using fed batch culture to optimize bacterial growth resulted is an increase in cell mass and consequently Vi production. The yield of Vi obtained in fed batch culture was 415 mg l⁻¹, which was over three times that, obtained in batch culture. A proportion of the Vi remained cell associated in the form of a capsule and at least part of this was released from the bacterial surface by sonication. The size of the Vi polysaccharide produced was consistently high and did not change during the different phases of bacterial growth. The synthesis of Vi was also dependent upon the media components and the fermentation conditions. The presence of high concentrations of glucose at the beginning of growth inhibited the production of Vi, particularly during the stationary phase. At a concentration of 400 mM sodium phosphate the synthesis of Vi was strongly inhibited.     

Short-term primary culture of mouse interstitial cells: effects of culture conditions of androgen production

This study examined the effects of culture conditions and hormone treatment on androgen production by mouse interstitial cells in short-term primary culture. Testicular interstitial cells (18-25% 3 beta-hydroxysteriod dehydrogenase-positive) were maintained in serum-free hormone supplemented medium. Basal (nonstimulated) androgen production was found to be plating-density dependent. Androgen production per cell increased dramatically in a time- and cell concentration-dependent manner. This effect was reproduced in low density cultures by addition of charcoal-stripped conditioned medium from high density cultures. The cell anchorage factors, fibronectin and poly-l-lysine, similarly enhanced basal androgen production but did not augment responsiveness to luteinizing hormone (LH). Coating of the culture surface with serum inhibited androgen production. Cultured cells remained responsive to LH for 4 to 5 days and both insulin (5 micrograms/ml) and epidermal growth factor (EGF) (3 ng/ml) augmented LH-stimulated androgen production. There was a transient increase in LH sensitivity and maximum LH-stimulated androgen production for 5 to 72 h in culture followed by a decline in androgen production to low levels after 4 to 5 days in culture. This loss of activity was partially prevented by addition of antioxidants to the medium or by reduction of the ambient O2 concentration to 1%.     

单克隆抗体Mab-A生产细胞Sp2/0缩小模型培养优化研究

Sp2/0是一种生产单克隆抗体的常用细胞株。本研究首先在批次培养模式中对适合Sp2/0细胞生长的5种基础培养基、摇床转速、培养温度、二氧化碳浓度、微量元素和GlutaMAX ^TM替换谷氨酰胺等影响因素进行了筛选研究。结果显示Sp2/0细胞在批次培养中细胞密度最高值达到13.12×10 ⁶ cells/ml,培养时间为7天。除培养温度会导致不同的细胞生长密度和活率、进而影响培养时间外,其它因素不能导致明显的细胞生长差异。随后在流加培养模式下就14种补料组合进行了筛选,Sp2/0在流加培养模式下细胞的峰值密度可达20~30×10 ⁶ cells/ml,培养时间9天,单克隆抗体Mab-A日产量最高达到27.20mg/L。最后应用批次-反复流加培养模式培养Sp2/0细胞,该条件下峰值细胞数为50.42×10 ⁶ cells/ml,培养时间14天,每天单抗产量(141.10mg/L)是流加培养的5.19倍。这些研究结果为Sp2/0细胞规模化生产单克隆抗体奠定了一定基础。     

High-density perfusion culture of insect cells with a biosep ultrasonic filter

The baculovirus/insect cell expression system has provided a vital tool to produce a high level of active proteins for many applications. We have developed a very high-density insect cell perfusion process with an ultrasonic filter as a cell retention device. The separation efficiency of the filter was studied under various operating conditions. A cell density of over 30 million cells/mL was achieved in a controlled perfusion bioreactor and cell viability remained greater than 90%. Sf9 cells from a high-density culture and a spinner culture were infected with two recombinant baculoviruses expressing genes for the production of human chitinase and monocyte-colony inhibition factor. The protein yield on a cell basis from infecting high-density Sf9 cells was the same as or higher than that from the spinner Sf9 culture. Virus production from the high-density culture was similar to that from the spinner culture. The results show that the ultrasonic filter did not affect insect cells' ability to support protein expression and virus production following infection with baculovirus. The potential applications of the high-density perfusion culture for large-scale protein expression from Sf9 cells are also highlighted.     

Production of L-DOPA from cell suspension culture of Mucuna pruriens f. pruriens

Summary Production of L-DOPA was studied in cell suspension culture of Mucuna pruriens f. pruriens. Suspension culture was established in MSI medium composed of half concentration of Murashige and Skoog's salts and 2% sucrose. A two-stage cell suspension culture was developed for enhanced accumulation of L-DOPA. In the first stage, the culture system was composed of MSI medium without CaCl, which was suitable for cell growth and in the second stage MSI medium containing 42.5 mg.l^–1 KH₂PO₄ and 4% sucrose favoured L-DOPA production. A discernible higher production of L-DOPA was obtained in this two-stage cell suspension culture in comparison to single stage culture.     

Effect of Nitrogen on Polysaccharide Production in a Porphyridium sp

Porphyridium cultures grown on either nitrate or ammonium as the nitrogen source showed similar patterns of growth and cell wall polysaccharide production. The effect of nitrogen on growth and cell wall polysaccharide production was studied by applying three regimens of supply: batch mode, in which nitrate was supplied at the beginning of the experiment and became depleted at day 6; continual mode, in which nitrate was added daily; and deficient mode, in which the cells were cultured in a nitrate-free medium. Growth was similar in the batch- and continual-mode cultures, whereas it was totally inhibited in the deficient-mode culture. Polysaccharide content (per volume) was highest in the batch-mode culture and lowest in the deficient-mode culture. However, polysaccharide production per cell was similar in the continual- and deficient-mode cultures, the highest value being found in the batch-mode culture. In addition to its effect on polysaccharide content, nitrogen affected the polysaccharide distribution between soluble and bound polysaccharides. In the deficientmode culture, most of the cell wall polysaccharide was dissolved in the medium.     

Enhanced kefiran production by mixed culture of Lactobacillus kefiranofaciens and Saccharomyces cerevisiae

In a batch mixed culture of Lactobacillus kefiranofaciens and Saccharomyces cerevisiae, which could assimilate lactic acid, cell growth and kefiran production rates of L. kefiranofaciens significantly increased, compared with those in pure cultures. The kefiran production rate was 36 mg l(-1) h(-1) in the mixed culture under the anaerobic condition, which was greater than that in the pure culture (24 mg l(-1) h(-1)). Under the aerobic condition, a more intensive interaction between these two strains was observed and higher kefiran production rate (44 mg l(-1) h(-1)) was obtained compared with that under the anaerobic condition. Kefiran production was further enhanced by an addition of fresh medium in the fed-batch mixed culture. In the fed-batch mixed culture, a final kefiran concentration of 5.41 g l(-1) was achieved at 87 h, thereby attaining the highest productivity at 62 mg l(-1) h(-1). Simulation study considered the reduction of lactic acid in pure culture was performed to estimate the additional effect of coculture with S. cerevisiae. Slightly higher cell growth and kefiran production rates in the mixed culture than those expected from pure culture by simulation were observed. These results suggest that coculture of L. kefiranofaciens and S. cerevisiae not only reduces the lactic acid concentration by consumption but also stimulates cell growth and kefiran production of L. kefiranofaciens.